201213532 六、發明說明： [發明所屬之技術領域】 本發明係關於一種季戊四醇（pentaerythritol)四 酯，係用於冷凍機油（Refrigerant Oil)等工業用潤滑油。 【先前技術】 近年來，係將臭氧破壞係數為零，且全球暖化潛勢 (GWP ; Global Warming Potential)更為低之氫氟碳化物 (HFC; Hydrofluorocarbon)作為冷凍機用之冷媒。二氟甲 烷冷煤（HFC-32)之GWP係較現今所用的冷媒[R-410A(二氟 甲烷與五氟乙烷之混合物）、R-407C(二氟甲烷、五氟乙烷 與1，1，1，2-四氟乙烧之混合物）等]低約1 /3至1 /4，且性 能係數（COP ; Coefficient Of Performance)亦相對於 R-410A、R-407C等約提升5至13%，故從節能化之觀點來 看為較佳之冷煤（非專利文獻1)。 於專利文獻1雖揭示用於二氟甲院冷煤用冷束機油之 季戊四醇與脂肪酸的酯，惟該酯對於二氟曱烷冷煤的相溶 性為不充分。 於專利文獻2雖記載使季戊四醇與異壬酸與異丁酸酐 以1 . 3 · 〇.5之莫耳比反應，所得之混合酯用以使含有陶 二、弓丨擎潤滑之方法，惟並未記載或提及該混合酯對於二 氣甲燒冷煤的相溶性。 [先月技術文獻] [專利文獻] [專利文獻1]曰本特開2002-129177號公報 323264 3 201213532 [專利文獻2]日本特開2004-43821號公報 [非專利文獻] [非專利文獻1]「潤滑經濟」，2004年6月號（No. 460)， P. 17 【發明内容】 (發明欲解決之課題） 本發明之目的在於係提供一種季戊四醇四酯，其係具 有對於二氟曱烷冷煤之優異相溶性等而用於冷凍機油 者。 (解決課題之手段） 本發明係提供以下[1]至[2]所記載的季戊四醇四酯。 [1] 一種季戊四醇四酯，其係季戊四醇與由異丁酸及 ’ 5, 5 一甲基己i所成的幾酸之混合酯，前述幾酸中相對 於3’5,5-三甲基己酸之異丁酸的莫耳比（異丁酸/3,5,5_三 甲基己酸比）為36/64至80/20的範圍。 [2] 如[1]所述之季戊四醇四酯，前述羧酸中相對於 3’5, 5-三甲基己酸之異丁酸的莫耳比（異丁酸/3, 5, 三甲 基己酸比）為36/64至67/33的範圍。 (發明之效果） 藉由本發明，係可提供具有對於二氟？炫冷煤之優異 相溶性等而用於冷凌機油等之季戊四醇四醋。 、 【實施方式】 以下，對本發明之較佳實施型態進行說明。 本發明之季戊四醇四酯係季戊四醇與由異丁酸及 323264 4 201213532 3, 5, 5-三曱基己酸所成的羧酸之混合酯，前述羧酸中相對 於3, 5, 5-三甲基己酸之異丁酸的莫耳比（異丁酸/3, 5, 5_三 曱基己酸比）為36/64至80/20的範圍，其中又以36/64至 67/33的範圍為較佳。但是，本發明亦包含為此範圍之外 而顯出本發明之效果的情形。於此，季戊四醇四酯係意指 季戊四醇的四個羥基以4分子之羧酸完全酯化而得之化合 物。 本發明之「混合酯」包含下述（i)至（iii)之各態樣： (i) 一種季戊四醇四酯，其同一分子中之構成羧酸係 由異丁酸及3, 5, 5-三甲基己酸兩者所成。 (ii) 一種酯混合物，其係混合季戊四醇與異丁酸的酯 以及季戊四醇與3, 5, 5-三曱基己酸的酯。 (ill) 一種混合物’其係上述（丨）及（ii)的混合物。 此外，本發明之季戊四醇四酯中亦可包含作為雜質之 季戊四醇三酯等。 本發明之季戊四醇四酯係可依所期望而於觸媒存在 下，將季戊四醇、異丁酸與3,5, 5_三曱基己酸以12〇至25〇 C使反應5至60小時而製造。 以觸媒而言，可列舉例如礦酸、有機酸、路易斯酸、 有機金屬、固體酸等。以礦酸的具體例而言，可列舉例如 ^氣I酸、硫酸、鱗酸、硝酸等。以有機酸的具體例 而言，可列舉例如對曱苯磺酸、苯磺酸、丁烷磺酸、乙烷 嶒馱、曱烷磺酸等。以路易斯酸的具體例而言，可列舉例 如二氟化硼、氯化鋁、四氯化錫、四氯化鈦等。以有機金 323264 5 201213532 屬的具體例而言，可列舉例如四丙氧鈦、四丁氧鈦肆U- 乙基己基氧基）鈦等。以固體酸的具體例而言，可舉例如陽 離子交換樹脂。 異丁酸的使用量與3, 5, 5-三曱基己酸的使用量之和， 相對於使用之季戊四醇的羥基，較佳為M至14倍莫耳。 月，j述反應係以-面自反應混合物取除由於反應而產生 的水、-面進行反應為較佳。自反應混合物取除由於反應 而產生的水時，有時亦會同時將異丁酸自反混合物取除。 前述反應係可於反應器附加精顧塔’而自反應混合物 取除由於反應而產生的水。附加精解而自反應混合物取 除由於反應而產生的水時，可調整該精鱗的運作條件以 使異丁酸的蒸騰量變化，藉此調整構成本發明之季戊四醇 四酯的異丁酸比率。 w於則述反應係可使用溶媒，以溶媒而言，可列舉例如： 笨甲笨、二曱苯、己烧、庚燒、異己燒、異辛烧、異壬 坑二癸垸等烴系溶媒等。藉由使用溶媒，可有效地自反應 -物取除由於反應而產生的水，而可縮短反應時間。 反應後，可因應所需而將本發明之季戊四醇四醋以一 般用於有機合成化學的方法（使用水及/或鹼性水溶液予以 洗淨，以活性碳、吸附劑等進行處理，各種管柱層析法、 蒸餾法等）予以精製。 本發明之季戊四醇四酯係具有對於二氟曱烷冷煤為優 異的相溶性、優異的低溫流動性、對於水解之優異的安定 性、優異的潤滑性等。 323264 ⑧ 201213532 當本發明之季戊四醇四酯用於空調機用冷;東機油日夺 該季戊四醇四醋於40°C之動黏度以20至70細!2/秒之範_ 較佳’以40至70mm2/秒之範圍為更佳。二層分離溫产 (two-layer separation temperature)以-15。。以下’佳 流動點（Pour point)以-40°C以下較佳，~42 5¾ α Γ馬更 佳。 本發明之季戊四醇四酯除了用於冷凍機油以外，亦可 用於機油（Engine oil)、齒輪油（Gear oi η 、ΒΒ 1J、潤滑脂 (Grease)、塑化劑等。 以使用本發明之季戊四醇四酯的冷康機油而古，。 舉如含有本發明之季戊四醇四醋與潤滑油用添加劑的冷= 機油。使用本發明之季戊四醇四酯的冷凍機油中，7 ζ γ，該四酉旨 係作為潤滑油基油使用。 以潤滑油用添加劑而言，可列舉例如：抗氧化气 、、 磨耗劑（耐磨耗劑、抗燃燒劑、極壓劑等）、摩挺調整、丨咸 酸捕捉劑（Acid Scavenger)、金屬減活劑、消泡劑等 & 用以作為潤滑油添加劑者。此等添加劑於冷來機、、由 又 佳含量，較佳分別為0.001至5重量％。 ' 乂 、本發明之季戊四醇四酯係可與其他潤滑油基油併用 以其他潤滑油基油而言，可列舉例如礦物油、合成基油等。 以礦物油而言’可列舉例如石蠟基系原油、中間基系 原油、環烷基系原油（Naphthene base crude oil)等。此 外，亦可使用將此等藉由蒸餾等進行精製的精製油。 以合成基油而言，可列舉例如聚-α-烯烴（聚丁烯、聚 7 323264 201213532 丙烯、碳數8至14的α-烯烴寡聚物等）、本發明之季戊四 醇四酯以外的脂肪族酯（脂肪酸單酯、多元醇的脂肪酸酯、 脂肪族多元酸酯等）、芳香族酯（芳香族單酯、多元醇的芳 香族酯、芳香族多元酸酯等）、聚烷二醇、聚乙烯醚、聚苯 醚、烷基苯、碳酸酯、合成環烷等。 此外，本發明之季戊四醇四酯對於苯并***等金屬減 活劑、聚矽氧系消泡劑等潤滑油用添加劑的溶解能力優 異。該潤滑油用添加劑可用於例如為了使潤滑油、使用潤 滑油的機器等的壽命延長，而溶解於潤滑油使用。該潤滑 油用添加劑一般而言對於季戊四醇酯之溶解性為低（曰本 特開平10-259394號公報）。此外，苯并***對於礦物油及 /或合成油之溶解度為低（日本特開昭59-189195號公 報）。然而，例如本發明之季戊四醇四酯之酯1(後述實施 例1)及酯6(後述實施例6)中之苯并***的溶解度（25°C) 為0. 005 g/g以上，任一之季戊四醇四酯皆表現出苯并三 唑的高溶解度。當使本發明之季戊四醇四酯溶解有苯并三 β坐時，係具有優異的低溫流動性、優異的财磨耗性。 此外，當將本發明之季戊四醇四酯作為潤滑油使用後 的機器於洗淨時，可藉由氟系清潔劑、醇系清潔劑等清潔 劑而輕易地將機器洗淨。 (.實施例）.. . 以下雖藉由實施例、參考例及試驗例，對本發明進行 更具體之說明，然不限定於以下之實施例。 分別測定以下之實施例1至11及參考例1至2所製造 8 323264 ⑧ 201213532 > 之季戊四醇四醋之核磁共振光譜，並藉由以下之式算出季 .戊四醇四酯的異丁酸與3, 5, 5-三曱基己酸之莫耳比。 核磁共振光譜係藉由以下之測定機器、測定方式而進 行測定。 測定機器：日本電子公司製GSX-400(400MHz) 測定方式：1H-丽R ’標準物質（四曱基石夕烧），溶媒 (CDC13) 異丁酸/3, 5, 5-三曱基己酸=峰X之積分值/峰γ之積分 值 在此，峰X相當於異丁酸之次甲基上的氫原子峰，峰 Y相當於3, 5, 5-三甲基己酸之次曱基上的氫原子峰。 [實施例1 :異丁酸與3, 5, 5-三甲基己酸之莫耳比（異丁酸 /3, 5, 5-二曱基己酸比）為39/61之季戊四醇四g旨（四g旨1) 的製造] 吸附劑係使用協和化學工業公司製之Ky〇waad 500。 活性碳係使用Japan EnviroChemicals公司製之白鷺 P ° 將季戊四醇1634g(12.0莫耳，Κ0ΕΙ PERST0RP公司 製）、異丁酸1979g(22. 5莫耳，東京化成公司製）及3, 5, 5_ 二甲基己酸5560g(35. 1莫耳，協和發酵化學股份有限公司 製）裝入到附有迪安-斯塔克分離器（Dean_Stark Trap)之 反應器中，藉由一面授拌混合物一面以室溫進行30分鐘氮 起泡（Nitrogen bubbling)而使混合物脫氣。 接下來，一面進行氮起泡一面將混合物以155至23〇 323264 9 201213532 °(：進行攪拌12. 5小時’接下來添加四丁氧基鈦至反應混合 、 物中，接著，以230°C攪拌反應混合物12小時。反應後， 藉由將反應生成物在l.lkPa的減壓下以225。(：攪拌1小 時，餾除反應生成物中未反應的羧酸。以2公升（L)包含相 對於該反應生成物的酸價為2倍莫耳的氩氧化鈉的鹼性水 溶液’將反應生成物以77°C進行洗淨1小時。接下來，將 反應生成物以2L水進行68°C之1小時的洗淨3次。接著， 藉由一面進行氮起泡一面將反應生成物於l lkPa的減壓 下以68°C攪拌1小時以乾燥反應生成物。 於反應生成物中添加吸附劑14ig(相當於反應生成物 的2重量％)及活性碳I4lg(相當於反應生成物的2重量％)， 一面進行氮起泡一面將反應生成物於l.3kPa.的減壓下以 110°C搅拌2小時後，藉由使用助濾劑進行過濾而得到 6402g之四酯1 〇 [實施例2 :異丁酸與3 5, 5_三曱基己酸之莫耳比（異丁酸 /3, 5, 5-二甲基己酸比）為36/64之季戊四醇四酯（四酯2) 的製造] 除了季戊四醇、異丁酸及3, 5, 5_三甲基己酸之使用量 的莫耳比（季戊四醇/異丁酸/3, 5, 5_三甲基己酸比）為 1/1.73/3.07以外’與實施例1以同樣方式進行操作，得 到四酯2。 • · .201213532 SUMMARY OF THE INVENTION [Technical Field] The present invention relates to a pentaerythritol tetraester which is used in industrial lubricating oils such as refrigerant oil. [Prior Art] In recent years, hydrofluorocarbons (HFCs), which have a low ozone destruction coefficient and a lower global warming potential (GWP), are used as refrigerants for refrigerators. The GWP of difluoromethane cold coal (HFC-32) is more than the refrigerant used today [R-410A (mixture of difluoromethane and pentafluoroethane), R-407C (difluoromethane, pentafluoroethane and 1, 1,1,2-tetrafluoroethane mixture), etc.] is about 1/3 to 1/4 lower, and the coefficient of performance (COP; Coefficient Of Performance) is also increased by about 5 to R-410A, R-407C, etc. Since it is 13%, it is a cold coal which is preferable from the viewpoint of energy saving (Non-Patent Document 1). Patent Document 1 discloses an ester of pentaerythritol and a fatty acid used in a cold-warm motor oil for cold coal of a difluorocarbon house, but the compatibility of the ester with difluorodecane cold coal is insufficient. In Patent Document 2, it is described that pentaerythritol is reacted with isophthalic acid and isobutyric anhydride at a molar ratio of 1.3 to 0.5, and the obtained mixed ester is used for the method of lubricating the ceramic containing the second and the second. The compatibility of the mixed ester with the second gas calcined cold coal is not described or mentioned. [Patent Document 1] [Patent Document 1] JP-A-2002-129177A 323264 3 201213532 [Patent Document 2] JP-A-2004-43821 [Non-Patent Document] [Non-Patent Document 1] "Lubrication Economy", June 2004 (No. 460), P. 17 [Disclosed] The object of the present invention is to provide a pentaerythritol tetraester having a difluorodecane It is used for refrigeration engine oils such as excellent compatibility of cold coal. (Means for Solving the Problem) The present invention provides the pentaerythritol tetraester described in the following [1] to [2]. [1] A pentaerythritol tetraester which is a mixed ester of pentaerythritol and a few acids formed from isobutyric acid and '5,5-methylhexan, which is relative to 3'5,5-trimethyl. The molar ratio of isobutyric acid (isobutyric acid / 3,5,5-trimethylhexanoic acid) is in the range of 36/64 to 80/20. [2] The pentaerythritol tetraester according to [1], the molar ratio of the above carboxylic acid to isobutyric acid of 3'5,5-trimethylhexanoic acid (isobutyric acid / 3, 5, trimethyl The ratio of hexanoic acid is in the range of 36/64 to 67/33. (Effects of the Invention) By the present invention, it is possible to provide for having difluoro? It is used for the pentaerythritol tetraacetic acid of cold engine oil, etc., because of its excellent compatibility with cold coal. [Embodiment] Hereinafter, preferred embodiments of the present invention will be described. The pentaerythritol tetraester of the present invention is a mixed ester of pentaerythritol with carboxylic acid formed from isobutyric acid and 323264 4 201213532 3, 5, 5-tridecylhexanoic acid, and the above carboxylic acid is relative to 3, 5, 5-tri The molar ratio of isobutyric acid to isobutyric acid (isobutyric acid / 3, 5, 5 - tridecylhexanoic acid ratio) is in the range of 36/64 to 80/20, which in turn is 36/64 to 67/ The range of 33 is preferred. However, the present invention also encompasses the case where the effects of the present invention are exhibited outside this range. Here, the pentaerythritol tetraester means a compound obtained by completely esterifying four hydroxyl groups of pentaerythritol with a tetracarboxylic acid. The "mixed ester" of the present invention comprises the following aspects (i) to (iii): (i) a pentaerythritol tetraester in which the constituent carboxylic acid is composed of isobutyric acid and 3, 5, 5- Made of trimethylhexanoic acid. (ii) an ester mixture which is an ester of pentaerythritol and isobutyric acid and an ester of pentaerythritol and 3,5,5-tridecylhexanoic acid. (ill) A mixture which is a mixture of the above (丨) and (ii). Further, the pentaerythritol tetraester of the present invention may contain a pentaerythritol triester or the like as an impurity. The pentaerythritol tetraester of the present invention can react with pentaerythritol, isobutyric acid and 3,5,5-tridecylhexanoic acid at 12 to 25 ° C for 5 to 60 hours in the presence of a catalyst as desired. Manufacturing. Examples of the catalyst include mineral acid, organic acid, Lewis acid, organic metal, solid acid, and the like. Specific examples of the mineral acid include, for example, gas I acid, sulfuric acid, scaly acid, nitric acid, and the like. Specific examples of the organic acid include p-toluenesulfonic acid, benzenesulfonic acid, butanesulfonic acid, ethane hydrazine, and decane sulfonic acid. Specific examples of the Lewis acid include, for example, boron difluoride, aluminum chloride, tin tetrachloride, and titanium tetrachloride. Specific examples of the genus of organic gold 323264 5 201213532 include, for example, titanium tetrapropoxide, titanium tetrabutoxide, U-ethylhexyloxy) titanium, and the like. Specific examples of the solid acid include a cation exchange resin. The sum of the amount of isobutyric acid used and the amount of 3,5,5-tridecylhexanoic acid used is preferably M to 14 times the molar amount of the hydroxyl group of the pentaerythritol to be used. In the month, it is preferred that the reaction is carried out by removing the water generated by the reaction from the reaction mixture on the surface. When the water produced by the reaction is removed from the reaction mixture, the isobutyric acid self-reverse mixture is sometimes removed. The foregoing reaction system can remove water generated by the reaction from the reaction mixture by adding the watch tower to the reactor. When the water produced by the reaction is removed from the reaction mixture by additional refinement, the operating conditions of the fine scale can be adjusted to change the transpiration of isobutyric acid, thereby adjusting the isobutyric acid ratio of the pentaerythritol tetraester constituting the present invention. . The solvent may be a reaction medium, and examples of the solvent include a hydrocarbon-based solvent such as a stupid, a diphenyl, a hexanyl, a heptane, an isohexan, an isooctane, or a diterpene. Wait. By using a solvent, water generated by the reaction can be effectively removed from the reaction, and the reaction time can be shortened. After the reaction, the pentaerythritol tetraacetic acid of the present invention can be used in accordance with a method generally used for organic synthetic chemistry (using water and/or an aqueous alkaline solution, and treated with activated carbon, adsorbent, etc., various columns). Purification by chromatography, distillation, etc.). The pentaerythritol tetraester of the present invention has excellent compatibility with difluorodecane cold coal, excellent low-temperature fluidity, excellent stability to hydrolysis, and excellent lubricity. 323264 8 201213532 When the pentaerythritol tetraester of the present invention is used for cooling of an air conditioner; the east engine oil takes the dynamic viscosity of the pentaerythritol tetraacetate at 40 ° C to 20 to 70 fine! 2 / sec _ better 'to 40 to The range of 70 mm 2 / sec is better. The two-layer separation temperature is -15. . The following 'good Pour points' are preferably below -40 °C, and ~42 53⁄4 α is better. The pentaerythritol tetraester of the present invention can be used not only for refrigerating machine oil but also for engine oil, gear oil (Gear oi η, ΒΒ 1J, grease (Grease), plasticizer, etc.) to use the pentaerythritol IV of the present invention. The cold-cold engine oil of the ester is as follows: a cold oil containing the pentaerythritol tetraacetate of the present invention and an additive for lubricating oil. In the refrigerating machine oil using the pentaerythritol tetraester of the present invention, 7 ζ γ, For the lubricating oil base, for example, an antioxidant gas, an anti-wear agent (a wear-resistant agent, an anti-burning agent, an extreme pressure agent, etc.), a friction adjustment, and a salty acid trapping agent are mentioned. (Acid Scavenger), metal deactivator, antifoaming agent, etc. & used as a lubricant additive. These additives are preferably 0.001 to 5% by weight, respectively, in a cold machine. The pentaerythritol tetraester of the present invention may be used together with other lubricating base oils for other lubricating base oils, for example, mineral oils, synthetic base oils, etc. In the case of mineral oils, for example, paraffin-based crude oils may be mentioned. in Further, a crude oil, a naphthene base crude oil, or the like may be used. Further, a refined oil which is purified by distillation or the like may be used. Examples of the synthetic base oil include poly-α- An olefin (polybutene, poly 7 323264 201213532 propylene, an α-olefin oligomer having 8 to 14 carbon atoms, etc.), an aliphatic ester other than the pentaerythritol tetraester of the present invention (a fatty acid monoester, a fatty acid ester of a polyhydric alcohol, An aliphatic polybasic acid ester, etc., an aromatic ester (an aromatic monoester, an aromatic ester of a polyhydric alcohol, an aromatic polybasic acid ester, etc.), a polyalkylene glycol, a polyvinyl ether, a polyphenylene ether, an alkylbenzene, a carbonic acid Further, the pentaerythritol tetraester of the present invention is excellent in the dissolving ability of an additive for lubricating oil such as a metal deactivator such as benzotriazole or a polyfluorene-based antifoaming agent. For example, in order to extend the life of a lubricating oil, a machine using a lubricating oil, or the like, it is dissolved in a lubricating oil. The additive for lubricating oil is generally low in solubility to pentaerythritol ester (JP-A-10-lane No. 10-259394) . In addition, the solubility of the benzotriazole in the mineral oil and/or the synthetic oil is low (JP-A-59-189195). However, for example, the ester of the pentaerythritol tetraester of the present invention (Example 1 described later) and the ester The solubility (25 ° C) of benzotriazole in 6 (Example 6 described later) is 0.005 g / g or more, and any of the pentaerythritol tetraesters exhibit high solubility of benzotriazole. When the pentaerythritol tetraester is dissolved in the benzotriazine, it has excellent low-temperature fluidity and excellent curability. Further, when the pentaerythritol tetraester of the present invention is used as a lubricating oil, it can be washed. The machine is easily washed by a cleaning agent such as a fluorine-based detergent or an alcohol-based detergent. (Examples) The present invention will be more specifically described below by way of Examples, Reference Examples and Test Examples, but is not limited to the examples below. The nuclear magnetic resonance spectra of pentaerythritol tetraacetate manufactured by the following Examples 1 to 11 and Reference Examples 1 to 2 were determined, and the isobutyric acid of the pentylenetetraol tetraester was calculated by the following formula. Mohr ratio with 3, 5, 5-tridecylhexanoic acid. The nuclear magnetic resonance spectrum was measured by the following measuring apparatus and measurement method. Measuring machine: GSX-400 (400MHz) manufactured by JEOL Ltd. Measurement method: 1H-Li R 'standard material (tetradecyl sulphate), solvent (CDC13) isobutyric acid / 3, 5, 5-tridecylhexanoic acid = integral value of peak X / integral value of peak γ Here, peak X corresponds to a hydrogen atom peak on the methine group of isobutyric acid, and peak Y corresponds to 3, 5, 5-trimethylhexanoic acid. The hydrogen atom peak on the base. [Example 1 : molar ratio of isobutyric acid to 3, 5, 5-trimethylhexanoic acid (isobutyric acid / 3, 5, 5-dimercaptohexanoic acid ratio) was 39/61 pentaerythritol tetrag Manufacture of (4 g) 1 The adsorbent was Ky〇waad 500 manufactured by Kyowa Chemical Industry Co., Ltd. For the activated carbon, Egret P° manufactured by Japan Enviro Chemicals Co., Ltd. used 1634 g of pentaerythritol (12.0 mol, Κ0ΕΙ PERST0RP), 1979 g of isobutyric acid (22.5 m, manufactured by Tokyo Chemical Industry Co., Ltd.), and 3, 5, 5_ dimethyl 5560 g of hexanoic acid (35. 1 mol, manufactured by Kyowa Fermentation Chemical Co., Ltd.) was charged into a reactor equipped with a Dean-Stark Trap, and the mixture was mixed with one side. Nitrogen bubbling was carried out for 30 minutes while the mixture was degassed. Next, while performing nitrogen bubbling while mixing the mixture at 155 to 23 〇 323264 9 201213532 ° (: stirring for 12.5 hours), then adding tetrabutoxy titanium to the reaction mixture, followed by 230 ° C The reaction mixture was stirred for 12 hours. After the reaction, the reaction product was reduced to 225 under a reduced pressure of 1.1 kPa. (: 1 hour, the unreacted carboxylic acid in the reaction product was distilled off. 2 liters (L) An alkaline aqueous solution containing sodium argon oxide having an acid value of 2 times the molar amount of the reaction product was washed with a reaction product at 77 ° C for 1 hour. Next, the reaction product was subjected to 2 L of water. The reaction product was washed three times at a temperature of 1 ° C. The reaction product was stirred at 68 ° C for 1 hour under reduced pressure of 1 lkPa while drying with nitrogen to dry the reaction product. The adsorbent 14ig (corresponding to 2% by weight of the reaction product) and the activated carbon I4lg (corresponding to 2% by weight of the reaction product) were added, and the reaction product was decompressed under a reduced pressure of 1.3 kPa while nitrogen was bubbled. After stirring at 110 ° C for 2 hours, it was obtained by filtration using a filter aid. 6402 g of tetraester 1 〇 [Example 2: molar ratio of isobutyric acid to 3 5,5-tridecylhexanoic acid (isobutyric acid / 3, 5, 5-dimethylhexanoic acid ratio) is 36 / Preparation of 64-pentaerythritol tetraester (tetraester 2)] In addition to the use of pentaerythritol, isobutyric acid and 3,5,5-trimethylhexanoic acid, the molar ratio (pentaerythritol / isobutyric acid / 3, 5, 5 The ratio of trimethylhexanoic acid to 1/1.73/3.07 was carried out in the same manner as in Example 1 to obtain a tetraester 2.
[實施例3 :異丁酸與3, 5, 5_三曱基己酸之莫耳比（異丁酸 /3’5, 5-二曱基己酸比）為37/63之季戊四醇四酯（四酯3) 的製造] 10 323264 ⑧ 201213532 除了季戊四醇、異丁酸及3,5, 5_三甲基己酸之使用量 的莫耳比（季戊四醇/異丁酸/3,5, 5一三甲基己酸比）為 1/1· 78/3. G2以外，與實施例丨關樣方式進行操作，得 到四酯3。 [實施例4 :異丁酸與3,5,5—三甲基己酸之莫耳比（異丁酸 /3,5,5-三甲基己酸比）為58/42之季戊四醇四酯（四醋 的製造] 除了季戊四醇、異丁酸及3, 5, 5_三甲基己酸之使用量 的莫耳比（季戊四醇/異丁酸/3,5,5_三甲基己酸比）為 1/2. 78/2. G2以外，與.實施例i以同樣方式進行操作，得 到四酯4。 [實施例5:異丁酸與3’5’5_三甲基己酸之莫耳比（異丁酸 /3’5’5-二甲基己_)為67/33之季細醇四 的製造] ) 除了季戊四醇、異丁酸及3, 5, 5—三甲基己酸之使用量 二莫二?(季戊四醇/異丁酸/3,5,5—三甲基己酸比)為 3·22/1.58以外’與實施例1以同樣方式進行操作，得 到四酯5。 ==列6:異丁酸與3,5,5_三甲基己酸之莫耳比（異丁酸 的製造Γ曱基己酸比）為76/24之季戊四醇四醋（四醋6) 除了季戊四醇、異τ酸及3,5,5_三甲基己酸之使用量 的莫耳比（季戊四醇/異了酸/3，仏 1/3.65/1.15以外，鱼實施你Μ以⑽&比）為 ，、貫苑例1以同樣方式進行操作，得 323264 11 201213532 到四S旨6。 [實施例7 :異丁酸蛊3 一田甘1 /、 ，5’5二曱基己酸之莫耳比（異丁酸 ，甲基己酸比）為80/20之季戊四醇四g|(四醋7) 的製造] 的莖Ϊ ^、異丁酸及3, 5,卜三甲基己酸之使用量 二二 /異丁酸/3,5,5-三甲基己酸比)為 .96以外，與實施例1以同樣方式進行操作，得 到四醋7。 =㈣8 :異丁酸與3,5,5—三甲基己酸之莫耳比（異丁酸 ’ ’甲基己酸比）為5G/5G之季戊四醇四醋(四醋 的製造] ； 除了季戊四醇、異丁酸及3, 5, 5_三曱基己酸之使用量 的莫耳比（季戊四醇/異丁酸/3, 5, 5-三甲基己酸比）為 1/2. 40/2. 4G以外，與實關丨以同樣方式進行操作， 到四酯8。 [實施例9 :異丁酸與3, 5,5_三甲基己酸之莫耳比（異丁酸 /3, 5’5-三甲基己酸比)為62/38之季戊四醇四酯(四 的製造] 除了季細醇、異丁酸及3, 5,卜三甲基己酸之使用量 的莫耳比（季戊四醇/異丁酸/3, 5,5_三甲基己酸比）為 1/2.98/1.82以外.，與實施例丨關樣方式進行操作，^ 到四酯9。 于 [實施例10:異丁酸與3, 5, 5-三曱基己酸之莫耳比（異丁酸 /3,5’5-三甲基己酸比）為64/36之季戊四醇四酯（四酯1〇) 323264 12 201213532 , 的製造] • 除了季戊四醇、異丁酸及3, 5, 5-三甲基己酸之使用量 的莫耳比（季戊四醇/異丁酸/3,5,5_三甲基己酸比）為 1/3.07/1.73以外’與實施例！以同樣方式進行操作 到四酯10。 [實施mi:異丁酸與3,5,5_三甲基己酸之莫耳比（異丁酸 /3’5,5-三曱基己酸比）為37/63之季戊四醇四酯 的製造] ~ 除了季戊四醇、異丁酸及3, 5, 5_三甲基己酸之使用量 的莫耳比（季戊四醇/異丁酸/3, 5, 5-三甲基己酸比）為 1/1.80/3.00，溶媒使用異辛烧（Ky〇was〇1 C 8〇〇 ;協和發 酵化學股份有限公㈣）以外，與實_丨以㈣方式 操作，得到四酯11。 [參考例_1 :異T酸與3,5,5_三甲基己酸之莫耳比（異丁酸 ，’5 _甲基己酸比）為24/76之季戊四醇四酯（四醋八） 的製造] 〜 除了使用異丁酸肝以取代異丁酸，季戊四醇、異丁酸 酐及3, 5, 5~三甲基己酸之使用量的莫耳比（季戊四醇/異丁 酸酐/3,5,5-三甲基己酸比）為1/〇5/3以外，與實施例1 以同樣方式進行操作，得到四酯A。 ^考例j ·異丁酸與3, 5, 5—三曱基己酸之莫耳比（異丁酸 ，5,5-三曱基己酸比）為84/16之季戊四醇四酯（四酯 的製造] 除了季戊四醇、異丁酸及3, 5, 5-三曱基己酸之使用量 323264 13 201213532 的莫耳比（季戊四醇/異丁酸/3, 5, 5-三曱基己酸比）為 1/4. 03/0.77以外，與實施例1以同樣方式進行操作，得 到四酯B。 [試驗例1 :流動點之測定] 使用自動流動點測定器RPP-01CML(離合公司製），依 照JIS K2269-1987之方法測定四酯1至10及A、B的流動 點。結果示於表1。 [試驗例2 :動黏度（Kinetic viscosity)之測定] 使用坎農-范斯克黏度計（音譯，Cannon-Fenske viscometer)，依照JIS K2283 : 2000之方法測定四酯1至 11及A、B在40°C的動黏度。結果示於表1及以下。 [試驗例3 :二層分離溫度之測定] 依照JIS K2211 : 2009之方法測定四酯1至1〇及a、 B的二層分離溫度。將四酯1至11及a、b各〇.4g與二氟 曱烷冷媒3. 6g封入耐壓玻璃管，將混合物從3yc以每分 鐘0.5°C之速度進行冷卻，將混合物二層分離或呈白濁時 的溫度作為二層分離溫度。結果示於表丨及以下。 [試驗例4 :於5°C之苯并***的溶解度之測定] 將〇· 15g苯并.三哇混合於各4. %的四醋i至1〇及A、 B中，以6ITC進行加熱，分別得到3重量％苯并三仙四醋 溶液。將該四醋溶液分別於5ΐ靜置4〇小時後，以目視進 行析出物的確認。 未見到析出物的該四醋溶液於代之苯并三唾的溶解 度[相對於18㈣之苯并三_容解量（g)]狀謂g/g以 323264 ⑧ 14 201213532 产上。[Example 3: The molar ratio of isobutyric acid to 3,5,5-tridecylhexanoic acid (isobutyric acid/3'5,5-dimercaptohexanoic acid ratio) was 37/63 pentaerythritol tetraester (Manufacture of tetraester 3)] 10 323264 8 201213532 In addition to the amount of pentaerythritol, isobutyric acid and 3,5,5-trimethylhexanoic acid used, it is a molar ratio (pentaerythritol / isobutyric acid / 3, 5, 5 The ratio of trimethylhexanoic acid was 1/1·78/3. Other than G2, it was operated in the same manner as in Example to obtain tetraester 3. [Example 4: The molar ratio of isobutyric acid to 3,5,5-trimethylhexanoic acid (isobutyric acid / 3,5,5-trimethylhexanoic acid ratio) was 58/42 pentaerythritol tetraester (Manufacturing of Four Vinegar) In addition to the molar ratio of pentaerythritol, isobutyric acid and 3,5,5-trimethylhexanoic acid (pentaerythritol / isobutyric acid / 3,5,5 - trimethylhexanoic acid ratio In the same manner as in Example i, except that 1/2.78/2. G2, tetraester 4 was obtained. [Example 5: isobutyric acid and 3'5'5-trimethylhexanoic acid Mohr ratio (isobutyric acid/3'5'5-dimethylhexan) is a 67/33 season of the manufacture of fine alcohols 4] except pentaerythritol, isobutyric acid and 3, 5, 5-trimethylhexyl The amount of the acid used was dimo-? (pentaerythritol / isobutyric acid / 3,5,5-trimethylhexanoic acid ratio) other than 3.22 / 1.58 - operation in the same manner as in Example 1 to obtain a tetraester 5 . ==Column 6: Mohr ratio of isobutyric acid to 3,5,5-trimethylhexanoic acid (the ratio of decylhexanoic acid produced by isobutyric acid) is 76/24 pentaerythritol tetraacetic acid (four vinegar 6) In addition to the molar ratio of pentaerythritol, isotonic acid and 3,5,5-trimethylhexanoic acid (pentaerythritol / iso-acid / 3, 仏 1/3.65 / 1.15, the fish implementation of (10) & In order to operate in the same way as in Example 1, 323264 11 201213532 to 4 S. [Example 7: 异3, Isobutyrate 3, and 5:5 dimercaptohexanoic acid molar ratio (isobutyric acid, methylhexanoic acid ratio) is 80/20 pentaerythritol tetrag | The manufacture of four vinegar 7)] stem Ϊ ^, isobutyric acid and 3, 5, b trimethyl hexanoic acid used in the amount of 22 / isobutyric acid / 3,5,5-trimethylhexanoic acid ratio) Other than .96, the same procedure as in Example 1 was carried out to obtain tetraacetate 7. = (4) 8: molar ratio of isobutyric acid to 3,5,5-trimethylhexanoic acid (isobutyric acid ''methylhexanoic acid ratio) is 5G/5G pentaerythritol tetraacetate (manufacture of tetravine vinegar); The molar ratio of pentaerythritol, isobutyric acid and 3,5,5-tridecylhexanoic acid (pentaerythritol / isobutyric acid / 3, 5, 5-trimethylhexanoic acid ratio) is 1/2. 40 In addition to /2. 4G, in the same manner as the real 丨, to the tetraester 8. [Example 9: Mohr ratio of isobutyric acid to 3,5,5-trimethylhexanoic acid (isobutyric acid / 3, 5'5-trimethylhexanoic acid ratio) is 62/38 pentaerythritol tetraester (manufacture of tetragen) except for the use of quaternary fine alcohol, isobutyric acid and 3, 5, trimethylhexanoic acid The ear ratio (pentaerythritol/isobutyric acid/3,5,5-trimethylhexanoic acid ratio) is 1/2.98/1.82. It is operated in the same manner as in the example, and is applied to the tetraester 9. Example 10: The molar ratio of isobutyric acid to 3,5,5-tridecylhexanoic acid (isobutyric acid/3,5'5-trimethylhexanoic acid ratio) is 64/36 pentaerythritol tetraester (four Ester 1〇) 323264 12 201213532 , Manufactured] • In addition to the use of pentaerythritol, isobutyric acid and 3, 5, 5-trimethylhexanoic acid, the molar ratio (season) The ratio of tetraol/isobutyric acid/3,5,5-trimethylhexanoic acid was 1/3.07/1.73' and the examples were carried out in the same manner to the tetraester 10. [Implemented mi: isobutyric acid and 3,5,5-trimethylhexanoic acid molar ratio (isobutyric acid / 3'5,5-trimercaptohexanoic acid ratio) is 37/63 of pentaerythritol tetraester] ~ except pentaerythritol, isobutyl The molar ratio of the acid and 3, 5, 5_ trimethylhexanoic acid used (pentaerythritol / isobutyric acid / 3, 5, 5-trimethylhexanoic acid ratio) is 1 / 1.80 / 3.00, the solvent used different In addition to Ky〇was〇1 C 8〇〇; Concord Fermentation Chemicals Co., Ltd. (4), it is operated in the same manner as in real (4) to obtain tetraester 11. [Reference Example_1: Iso-acid and 3,5 , 5_ trimethylhexanoic acid molar ratio (isobutyric acid, '5-methylhexanoic acid ratio) is 24/76 pentaerythritol tetraester (four vinegar) production] ~ In addition to the use of isobutyric acid liver The molar ratio (pentaerythritol / isobutyric anhydride / 3,5,5-trimethylhexanoic acid ratio) of pentaerythritol, isobutyric anhydride and 3, 5, 5 - trimethylhexanoic acid is substituted for isobutyric acid. In the same manner as in Example 1 except 1/〇5/3, tetraester A was obtained. The molar ratio of butyric acid to 3,5,5-tridecylhexanoic acid (isobutyric acid, 5,5-tridecylhexanoic acid ratio) is 84/16 pentaerythritol tetraester (manufacture of tetraester) except pentaerythritol Use of isobutyric acid and 3,5,5-tridecylhexanoic acid 323264 13 201213532 molar ratio (pentaerythritol / isobutyric acid / 3, 5, 5-tridecylhexanoic acid ratio) is 1/4 Other than Example 03/0.77, the same procedure as in Example 1 was carried out to obtain a tetraester B. [Test Example 1: Measurement of the flow point] The flow points of the tetraesters 1 to 10 and A and B were measured in accordance with the method of JIS K2269-1987 using an automatic flow point measuring device RPP-01CML (manufactured by Seiko Co., Ltd.). The results are shown in Table 1. [Test Example 2: Measurement of Kinetic viscosity] Using a Cannon-Fenske viscometer, tetraesters 1 to 11 and A and B were measured in accordance with JIS K2283:2000. Dynamic viscosity of °C. The results are shown in Table 1 and below. [Test Example 3: Measurement of the separation temperature of the two layers] The two-layer separation temperature of the tetraesters 1 to 1 and the a and B was measured in accordance with the method of JIS K2211:2009. 6 g of tetraesters 1 to 11 and a, b, and 4 g of difluorodecane refrigerant were sealed in a pressure-resistant glass tube, and the mixture was cooled from 3 yc at a rate of 0.5 ° C per minute, and the mixture was separated into two layers or The temperature at the time of white turbidity was taken as the separation temperature of the second layer. The results are shown in Tables and below. [Test Example 4: Determination of Solubility of Benzotriazole at 5 ° C] 〇·15 g of benzotriazine was mixed in each of 4.% of tetraacetin i to 1 Å and A and B, and 6ITC was carried out. Heating, respectively, gave a 3% by weight solution of benzotriazine. After the four vinegar solutions were allowed to stand at 5 Torr for 4 hrs, the precipitates were visually confirmed. The solubility of the tetraacetic acid solution in which the precipitate was not observed was replaced by the solubility of benzotriazine (relative to the amount of benzotriene (g) of 18 (four)], and g/g was produced as 323264 8 14 201213532.
見到析出物的該四酯溶液在藉由過濾（濾紙；No. 5A， 桐山製作所製）去除析出物後，以高速液體層析法（AGILENT 公司製 1200SERIES’ 管柱：YMC Pack Ph Α-414 φβ.Οχ 300mm)，移動相：四氫呋喃/〇. 1%磷酸水溶液=7/3，管柱溫 度：40°C ’流速：0. 7mL/分鐘’檢測：UV(200nm)，試樣濃 度：50g/L，注入（inject)量：5//L)測定所得到的濾液， 藉由絕對校準曲線法（Absolute calibration curve method)求得於5°C之苯并***的溶解度[相對於lg四酯之 苯并***的溶解（g)]。結果示於表2。 [試驗例5 :四酯溶液之磨耗痕徑之測定] 將0.20g苯并***混合於各19.80g的四酯1至10及 A、B中，以60°C進行加熱，分別得到笨并三峻的1重量％ 四酯溶液。 將所得到的該1重量％四酯溶液分別以Shell式四球試 驗機（Shell style four-ball tester)(神鋼造機公司製） 荷重200N，每分鐘旋轉數1200rpm，時間3〇分鐘，溫度 75°C，試驗材[試驗球（SUJ-2)]的條件進行試驗，測定試驗 後的磨耗痕徑。磨耗痕徑為3個固定球的垂直方向、水平 方向之總平均值。結果示於表2。 於表2之磨耗痕徑之值越小者，表示四酿溶液的耐磨 耗特性越為優異。 [試驗例6 :四酯溶液之流動點之測定] 將1. 35g苯并三唾混合於各43· 65g的四酿1至10及 15 323264 201213532 A、B中，以60°C進行加熱 四酉旨溶液。 分別得到笨并***的 3重量％ 使用自動流動點測定器RPP-01CML(離合公司製），依 照JIS K2269-1987之方法，分別測定該3重量％四酯溶液 的流點。結果示於表2。 於表2 ’ BZT係表示苯并三0坐。 [表1] 四酷 異丁酸/3, 3, 5-三曱基己酸比 動黏度 流動點 二層分離溫度 (莫耳比） (mm2/秒） rc) ΓΟ A(參考例1) 24/76 88. 2 -37. 5 -1 2(實施例2) 36/64 69. 5 -42. 5 -20 3(實施例3) 37/63 68. 9 -42. 5 -20 1(實施例1) 39/61 66. 3 -42. 5 -23 8(實施例8) 50/50 55. 2 -42. 5 -35 4(實施例4) 58/42 47. 7 -45. 0 -41 9(實施例9) 62/38 45. 7 -45. 0 -47 10(實施例1〇) 64/36 43. 6 -45. 0 S-50 5(實施例5) 67/33 40. 1 -45. 0 S -50 6(實施例6) 76/24 33. 9 -40. 0 客-50 7(實施例Ό 80/20 30. 6 -40. 0 S-50 B(參考例2) 84/16 27· 9 -20. 0 芸-50 16 323264 ⑧ 201213532 [表2] 四醋 異丁酸/3, 3, 5-三甲基己酸比 (莫耳比） 於5°C之BZT 的溶解度 (g/g) 磨耗痕徑（mm) 流動點rc) 1重量％ΒΖΤ 的四酯溶液 3重量96BZT 的四酯溶液 A(參考例1) 24/76 0. 014 0. 62 -17. 5 2(實施例2) 36/64 0. 021 0.49 -40. 〇 3(實施例3) 37/63 0. 020 0. 52 -40. 〇 1(實施例1) 39/61 0. 021 0. 54 -40. 0 8(實施例8) 50/50 0. 025 0. 60 -42. 5 4(實施例4) 58/42 0. 024 0. 56 -45. 0 9(實施例9) 62/38 ^0. 030 0. 57 -45 0 10(實施例10) 64/36 ^0.030 0. 55 '45. 0 5(實施例5) 67/33 含 0. 030 0. 55 -45· 〇 6(實施例6) 76/24 2 0· 030 0. 57 -47. 5 7(實施例7) 80/20 2 0.030 0. 60 -47. 5 B(參考例2) 84/16 ^ 0. 030 0. 55 -20. 〇 藉由表1，可瞭解到四酯丨至1〇於4(rc之動黏度為 3〇. 6至69. 5mmV秒，流動點為-40· 0至-45..0Ϊ且具有優異 的低溫流動性’二層分離溫度為-2(TC以下且具有對於二氟 曱烧冷煤之優異的相溶性。此外瞭解到，四丨至5、8至 10之流動點為-42.5至-45.0。(：且具有更為優異的低溫流 動性。四醋11之動黏度為68. W/秒，二層分離溫度為_2〇 °C，幾乎與實施例3同等。 藉由表2 ’可瞭解到則旨1至1G於5°c之苯并三唾溶 解度為0. G2Gg/g以上且溶解苯并三奴能力優異。此外， 因四酉曰1至1G之苯并二唾的3重量％四醋溶液的流動點為 323264 17 201213532 -40. 0°C以下，苯并***的1重量％四酯溶液之磨耗痕徑為 0. 60mm以下，故暸解到在使苯并***溶解時，係具有優異 的低溫流動性與優異的耐磨耗性。 (產業上之可利用性） 藉由本發明，係可提供一種季戊四醇四酯，其係具有 對於二氟曱烷冷煤之優異相溶性等而用於冷凍機油等者。 【圖式簡單說明】 無。 【主要元件符號說明】 無。 18 323264 ⑧The tetraester solution of the precipitate was removed by filtration (filter paper; No. 5A, manufactured by Kiriyama Seisakusho Co., Ltd.), and then subjected to high-speed liquid chromatography (1200 SERIES' column manufactured by AGILENT: YMC Pack Ph Α-414 Φβ.Οχ 300mm), mobile phase: tetrahydrofuran/〇. 1% phosphoric acid aqueous solution=7/3, column temperature: 40°C 'flow rate: 0. 7mL/min' detection: UV (200nm), sample concentration: 50g /L, inject amount: 5 / / L) The obtained filtrate was measured, and the solubility of benzotriazole at 5 ° C was determined by Absolute calibration curve method [relative to lg four Dissolution of the ester benzotriazole (g)]. The results are shown in Table 2. [Test Example 5: Measurement of abrasion scar diameter of tetraester solution] 0.20 g of benzotriazole was mixed in each of 19.80 g of tetraesters 1 to 10 and A and B, and heated at 60 ° C to obtain a stupid Sanjun's 1% by weight tetraester solution. The obtained 1% by weight tetraester solution was respectively subjected to a Shell style four-ball tester (manufactured by Kobelco Co., Ltd.) with a load of 200 N, a number of revolutions per minute of 1200 rpm, a time of 3 minutes, and a temperature of 75 ° C. The test material [test ball (SUJ-2)] was tested under the conditions of the test piece, and the wear scar diameter after the test was measured. The wear scar diameter is the total average value of the vertical direction and the horizontal direction of the three fixed balls. The results are shown in Table 2. The smaller the value of the wear scar diameter in Table 2, the more excellent the wear resistance characteristics of the four-brewed solution. [Test Example 6: Measurement of the flow point of the tetraester solution] 1. 35 g of benzotriazine was mixed in each of 43.65 g of four brews 1 to 10 and 15 323264 201213532 A, B, and heated at 60 ° C. The purpose of the solution. 3 wt% of the bismuth triazole solution was obtained by using an automatic flow point measuring device RPP-01 CML (manufactured by Seiko Co., Ltd.) in accordance with the method of JIS K2269-1987, and the flow point of the 3% by weight tetraester solution was measured. The results are shown in Table 2. In Table 2' BZT series indicates that benzotrim is sitting. [Table 1] Tetrahydroisobutyric acid/3,3,5-tridecylhexanoic acid specific viscosity flow point two-layer separation temperature (mol ratio) (mm2/sec) rc) ΓΟ A (Reference Example 1) 24 /76 88. 2 -37. 5 -1 2 (Example 2) 36/64 69. 5 -42. 5 -20 3 (Example 3) 37/63 68. 9 -42. 5 -20 1 (Implementation Example 1) 39/61 66. 3 - 42. 5 -23 8 (Example 8) 50/50 55. 2 - 42. 5 - 35 4 (Example 4) 58/42 47. 7 -45. 0 - 41 9 (Example 9) 62/38 45. 7 -45. 0 -47 10 (Example 1〇) 64/36 43. 6 -45. 0 S-50 5 (Example 5) 67/33 40. 1 -45. 0 S -50 6 (Example 6) 76/24 33. 9 -40. 0 Guest-50 7 (Example Ό 80/20 30. 6 -40. 0 S-50 B (Reference Example 2) 84/16 27· 9 -20. 0 芸-50 16 323264 8 201213532 [Table 2] Four acetoisobutyric acid / 3, 3, 5-trimethylhexanoic acid ratio (Morby) at 5 ° C Solubility of BZT (g/g) Wear scar diameter (mm) Flow point rc) 1% by weight 四 tetraester solution 3 weight 96BZT tetraester solution A (Reference Example 1) 24/76 0. 014 0. 62 -17 5 2 (Example 2) 36/64 0. 021 0.49 -40. 〇3 (Example 3) 37/63 0. 020 0. 52 -40. 〇1 (Example 1) 39/61 0. 021 0. 54 -40. 0 8 (Example 8) 50/5 0 0. 025 0. 60 -42. 5 4 (Example 4) 58/42 0. 024 0. 56 -45. 0 9 (Example 9) 62/38 ^0. 030 0. 57 -45 0 10 (Example 10) 64/36 ^0.030 0. 55 '45. 0 5 (Example 5) 67/33 Contains 0. 030 0. 55 -45· 〇 6 (Example 6) 76/24 2 0· 030 0. 57 -47. 5 7 (Example 7) 80/20 2 0.030 0. 60 -47. 5 B (Reference Example 2) 84/16 ^ 0. 030 0. 55 -20. 〇 By Table 1, It can be understood that tetraester 丨 to 1 〇 to 4 (rc has a dynamic viscosity of 3 〇. 6 to 69. 5 mmV seconds, a flow point of -40·0 to -45..0 Ϊ and excellent low-temperature fluidity 'two layers The separation temperature is -2 (TC or less and has excellent compatibility with difluoromethane-burned cold coal. In addition, it is understood that the flow point of four to five, 8 to 10 is -42.5 to -45.0. (: and has a better low-temperature fluidity. The dynamic viscosity of the four vinegar 11 is 68. W / sec, and the separation temperature of the second layer is _2 〇 ° C, which is almost equivalent to that of the embodiment 3. It can be understood from Table 2' The benzotriazole solubility at 5 ° C is 0. G2Gg / g or more and is excellent in dissolving benzotriene. In addition, 3% by weight of benzodiazepine of 4 酉曰 1 to 1G The flow point of the tetraacetic acid solution is 323264 17 201213532 -40. Below 0 ° C, the wear scar diameter of the 1 wt% tetraester solution of benzotriazole is 0. 60 mm or less, so it is known that when the benzotriazole is dissolved It has excellent low-temperature fluidity and excellent wear resistance. (Industrial Applicability) By the present invention, it is possible to provide a pentaerythritol tetraester which has excellent compatibility with difluorodecane cold coal. For refrigeration engine oil, etc. [Simple description of the diagram] None. [Main component symbol description] None. 18 323264 8